Single-step conversion of levulinic acid to valeric acid over bimetallic Ni-Co/H-ZSM-5 catalysts

被引:1
|
作者
Nagu, Ajmeera [1 ,2 ]
Raju, Ajmira [1 ,3 ]
Vennela, Aluvala [4 ]
Varkolu, Mohan [5 ]
Raju, Burri David
Rao, Kamaraju Seetha Rama [1 ]
机构
[1] Indian Inst Chem Technol, Catalysis & Fine Chem Div, CSIR, Hyderabad 500007, Telangana, India
[2] Indian Inst Technol Tirupati, Yerpedu Venkatagiri Rd,Yerpedu Post, Tirupati 517619, Andhra Pradesh, India
[3] Kakatiya Univ, Univ Arts & Sci Coll, Dept Phys, Hanamkonda 506001, Telangana, India
[4] Osmania Univ, Dept Chem, Amberpet, Hyderabad 500007, Telangana, India
[5] Koneru Lakshmaiah Educ Fdn, Dept Chem, Moinabad Rd,RVS Nagar,Azziz Nagar PO, Hyderabad 500075, Telangana, India
来源
CHEMISTRYSELECT | 2023年 / 8卷 / 20期
关键词
Biofuels; cobalt; nickel; valeric acid; zeolites; GAMMA-VALEROLACTONE; PHASE HYDROGENATION; SUPPORTED NI; BIOMASS; BIOFUELS; ESTERS; FUELS; PLATFORM;
D O I
10.1002/slct.202300509
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Single-step conversion of levulinic acid (LA) to valeric biofuel is extremely promising for the development of bio-refineries. Direct conversion of LA to valeric acid (VA) was investigated over H-ZSM-5 supported Ni, Co, and Ni-Co (different Ni/Co wt. % ratios) catalysts under ambient reaction conditions (543 K and atmospheric pressure) in the gas phase. Compared with supported monometallic catalysts, bimetallic Ni-Co catalysts exhibited more activity and selectivity toward VA production. Among Ni-Co/H-ZSM-5 catalysts, 15Ni-5Co/H-ZSM-5 catalyst is optimum with 97.5 % conversion of LA and 63 % selectivity to valeric acid even after 6 h time-on-stream (TOS). The active metallic sites are responsible for the hydrogenation of LA to gamma-valerolactone (GVL), and acidic sites catalyze the conversion of GVL to VA. All the catalysts were characterized using the XRD, H-2-TPR, N-2-adsorption-desorption isotherms, NH3-TPD, Py-IR, SEM, HR-TEM and XPS techniques.
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页数:10
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